Method and apparatus for automated, modular, biomass power generation
Method and apparatus for generating a low tar, renewable fuel gas from biomass and using it in other energy conversion devices, many of which were designed for use with gaseous and liquid fossil fuels. An automated, downdraft gasifier incorporates extensive air injection into the char bed to maintain the conditions that promote the destruction of residual tars. The resulting fuel gas and entrained char and ash are cooled in a special heat exchanger, and then continuously cleaned in a filter prior to usage in standalone as well as networked power systems.
1. An automated method for converting a solid, carbonaceous material to a low tar fuel gas within a downdraft gasification reactor chamber, comprising:
introducing the carbonaceous material into the chamber;
transforming a first portion of the carbonaceous material into a char material at a flaming pyrolysis zone;
controlling a plurality of temperatures along a length of the chamber by injecting oxidizing gas at more than two levels in the gasification reactor chamber, wherein:
the oxidizing gas is injected through a plurality of injection tubes that protrude radially through the gasification reactor chamber walls into the interior of the gasification reactor chamber,
the plurality of injection tubes protrude radially into the interior of the gasification reactor chamber at varying distances from the gasification reactor chamber walls,
each injection tube of the plurality of injection tubes comprises a plurality of nozzles through which the oxidizing gas is delivered, and
the plurality of injection tubes inject oxidizing as into the interior of the gasification reactor chamber at varying distances from the gasification reactor chamber walls;
controlling an amount of the oxidizing gas injected from at least one of the more than two-levels;
varying a location of the flaming pyrolysis zone within the chamber by increasing or decreasing an amount of oxidizing gas injected upstream or downstream of the pyrolysis zone;
controlling a porosity of the char material and a second portion of the carbonaceous material in the gasification reactor chamber by applying at least one force to the chamber; and
converting the char material and the second portion of the carbonaceous material to the low tar fuel gas within the gasification reactor chamber.
2. The method of claim 1 , further comprising controlling a temperature and the location of the flaming pyrolysis zone to maximize tar reduction for a prescribed range of fuel gas flow rates.
3. The method of claim 1 , further comprising controlling the porosity of the char material and the second portion of the carbonaceous material to maximize tar reduction with a minimum of pressure drop for a prescribed range of fuel gas flow rates.
4. The method of claim 1 , wherein the carbonaceous material comprises a bulk density of greater than about 3 pounds per cubic foot.
5. The method of claim 1 , wherein the carbonaceous material comprises one or more members selected from the group consisting of a woody biomass, a non-woody biomass, a cellulosic product, a cardboard, a fiber board, a paper, a plastic, and a food stuff.
6. The method of claim 1 , further comprising controlling the amount of oxidizing gas injected in the gasification chamber at two or more levels with one or more variable speed fans or blowers, with one or more valves, or with one or more flow restrictors.
7. The method of claim 1 , wherein applying at least one force to the chamber comprises applying a vibrational force to the chamber to collapse bridges and channels therein.
8. The method of claim 1 , wherein applying at least one force to the chamber comprises moving a grate located at a downstream outlet of the gasification reactor chamber, the grate configured to crush frangible char or ash to particles that are sized to pass through a mesh screen.
9. The method of claim 1 , further comprising:
reducing the char to a particle that is sized for entrainment in the low tar fuel gas downstream of a gasification reactor chamber;
entraining the char in the low tar fuel gas;
passing the fuel gas and entrained char through the inside of the tubes of a shell-and-tube heat exchanger to control the temperature of the fuel gas to promote collection of tar on the surface of the entrained char such that the entrained char becomes tar laden; and
filtering the fuel gas to remove the tar laden char particulates from the fuel gas.
10. The method of claim 9 , further comprising stress relieving the individual tubes of the shell-and-tube heat exchanger through individual seals in a tube sheet.
11. The method of claim 9 , wherein filtering the fuel gas comprises using a self cleaning filter, the self-cleaning filter providing for continuous operation.
12. The method of claim 1 , further comprising controlling an amount of the oxidizing gas injected through the injection tubes from more than two of the plurality of levels, wherein the oxidizing gas is injected roughly uniformly throughout the gasification reactor chamber to control the temperature throughout the gasification reactor chamber and thereby allow large diameter gasification reactor chambers to be used to make a low-tar fuel gas.
13. The method of claim 1 , further comprising coupling a temperature measuring device with at least one of the plurality of injection tubes.
14. The method of claim 13 , wherein coupling the temperature measuring device comprises inserting the temperature measuring device into a thermowell located at one end of the at least one of the plurality of injection tubes.
15. The method of claim 1 , further comprising controlling the temperature of the fuel gas to keep the fuel gas above its water dew-point temperature by controlling a pre-heating of a heat exchanger and filter system prior to igniting the gasification reactor chamber and by controlling the cooling of the fuel gas in the heat exchanger after ignition.
16. The method of claim 1 , further comprising controlling the gasification reactor chamber temperatures so as to avoid the need for high temperature refractory materials.
17. The method of claim 1 , wherein the plurality of injection tubes comprise a plurality of nozzles configured to deliver the oxidizing gas in a direction generally non-perpendicular to a direction of flow of the fuel gas.
18. The method of claim 17 , wherein the plurality of injection tubes are removable from the gasification reactor chamber, and wherein one of the plurality of injection tubes is removed for one or more of the following reasons:
inspection;
maintenance;
replacement with an injection tube having a different length, a different material, a different nozzle size, or a different nozzle spacing; and
igniting the carbonaceous material in the gasification reactor chamber.
19. The method of claim 2 , wherein controlling the location of the flaming pyrolysis zone comprises controlling either or both of the frequency and duration of char and ash removal by a movable grate located at a downstream outlet of the gasification reactor chamber.
20. An automated method for converting a solid, carbonaceous material to a low tar fuel gas within a downdraft gasification reactor chamber, comprising:
introducing the carbonaceous material into the chamber;
transforming a first portion of the carbonaceous material into a char material at a flaming pyrolysis zone;
controlling a plurality of temperatures along a length of the chamber by injecting oxidizing gas at more than two levels in the gasification reactor chamber, wherein:
the oxidizing gas is injected through a plurality of injection tubes that protrude radially through the gasification reactor chamber walls into the interior of the gasification reactor chamber,
the plurality of injection tubes protrude radially into the interior of the gasification reactor chamber at varying distances from the gasification reactor chamber walls,
each injection tube of the plurality of injection tubes comprises a plurality of nozzles through which the oxidizing gas is delivered, and
the plurality of injection tubes inject oxidizing gas into the interior of the gasification reactor chamber at varying distances from the gasification reactor chamber walls;
controlling an amount of the oxidizing gas injected from at least one of the more than two-levels;
varying a location of the flaming pyrolysis zone within the chamber by increasing or decreasing an amount of oxidizing gas injected upstream or downstream of the pyrolysis zone;
controlling a porosity of the char material and a second portion of the carbonaceous material in the gasification reactor chamber by applying at least one force to the chamber and the plurality of injection tubes to collapse channels and bridges within the chamber; and
converting the char material and the second portion of the carbonaceous material to the low tar fuel gas within the gasification reactor chamber.